Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
US12552080B2 - Planetary roller extruder for processing biodegradable materials and method for cleaning the planetary roller extruder - Google Patents
[go: Go Back, main page]

US12552080B2 - Planetary roller extruder for processing biodegradable materials and method for cleaning the planetary roller extruder - Google Patents

Planetary roller extruder for processing biodegradable materials and method for cleaning the planetary roller extruder

Info

Publication number
US12552080B2
US12552080B2 US18/695,818 US202218695818A US12552080B2 US 12552080 B2 US12552080 B2 US 12552080B2 US 202218695818 A US202218695818 A US 202218695818A US 12552080 B2 US12552080 B2 US 12552080B2
Authority
US
United States
Prior art keywords
planetary roller
roller extruder
flow
flow conduit
cleaning
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active, expires
Application number
US18/695,818
Other versions
US20250018631A1 (en
Inventor
Thomas Gesper
Heinrich Dohmann
Michael Kaiser
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Battenfeld Cincinnati Germany GmbH
Original Assignee
Battenfeld Cincinnati Germany GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Battenfeld Cincinnati Germany GmbH filed Critical Battenfeld Cincinnati Germany GmbH
Publication of US20250018631A1 publication Critical patent/US20250018631A1/en
Application granted granted Critical
Publication of US12552080B2 publication Critical patent/US12552080B2/en
Active legal-status Critical Current
Adjusted expiration legal-status Critical

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/34Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
    • B29B7/38Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
    • B29B7/46Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/48Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft with intermeshing devices, e.g. screws
    • B29B7/485Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft with intermeshing devices, e.g. screws with three or more shafts provided with screws
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/34Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
    • B29B7/38Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
    • B29B7/46Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/48Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft with intermeshing devices, e.g. screws
    • B29B7/488Parts, e.g. casings, sealings; Accessories, e.g. flow controlling or throttling devices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/80Component parts, details or accessories; Auxiliary operations
    • B29B7/802Constructions or methods for cleaning the mixing or kneading device
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/80Component parts, details or accessories; Auxiliary operations
    • B29B7/82Heating or cooling
    • B29B7/826Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/022Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the choice of material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/254Sealing means
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/27Cleaning; Purging; Avoiding contamination
    • B29C48/2715Cleaning; Purging; Avoiding contamination of plasticising units
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/375Plasticisers, homogenisers or feeders comprising two or more stages
    • B29C48/385Plasticisers, homogenisers or feeders comprising two or more stages using two or more serially arranged screws in separate barrels
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/395Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
    • B29C48/40Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
    • B29C48/435Sub-screws
    • B29C48/44Planetary screws
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/58Component parts, details or accessories; Auxiliary operations
    • B29B7/72Measuring, controlling or regulating
    • B29B7/728Measuring data of the driving system, e.g. torque, speed, power, vibration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2995/00Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
    • B29K2995/0037Other properties
    • B29K2995/0059Degradable
    • B29K2995/006Bio-degradable, e.g. bioabsorbable, bioresorbable or bioerodible

Definitions

  • the invention relates to a planetary roller extruder for homogenizing, dispersing, pasteurizing, and purposefully controlling the temperature of biodegradable materials that are prone to altering their properties during processing.
  • the invention also relates to a method for cleaning the planetary roller extruder.
  • planetary roller extruders it is well known to use planetary roller extruders to produce a plastics melt, preferably for the granulation process or for continuous film production.
  • a plurality of planetary spindles are arranged between a planetary roller cylinder and a central or main spindle.
  • the teeth set into the roller cylinders, planetary spindles, and central spindle roll on one another such that the plastics material to be gelled is subject to an intensive kneading action.
  • the plastics melt thus produced is of a high quality.
  • the functioning of a planetary roller extruder in terms of a process is determined substantially by the temperature control of the stationary outer casing of the planetary roller cylinder and of the rotating main spindle, since the high surface-area-to-volume ratio in this case can have a particularly effective impact on the preparation of the product.
  • the main field of application of the planetary roller extruder is in the preparation of shear- and temperature-sensitive materials, mainly PVC formulations, powder coating binder resins, and thermoplastic polyolefins (TPO). If excessively heated, PVC, for example, reacts by combusting and decomposing. The resulting so-called black spots lead to a considerable degradation in quality, particularly in the case of transparent mixtures or thin films. This problem is alleviated by setting low housing temperatures or by reducing the output by lowering the speeds, which of course results in corresponding efficiency losses.
  • Powder coatings have to be prepared at the lowest possible temperatures owing to the required dispersibility in pigmented formulations and the risk of crosslinking in transparent, clear formulations. In this case, local excessive heating can likewise accordingly impact on quality, or may render preparation entirely impossible. In this regard, it has been observed that with critical materials (e.g., soft PVC), degradation of the material due to decomposition occurred particularly at the downstream-facing end of the planetary roller component.
  • critical materials e.g., soft PVC
  • thermoplastic polyolefins When preparing thermoplastic polyolefins, the aim is to achieve uniform melting. For system-related reasons, only a relatively slight pressure can be built up in a planetary roller extruder compared with other preparation systems; this may be advantageous for other forms of preparation.
  • the goal is to make use of these significant advantages of a planetary roller extruder (good homogenization, good dispersal of the material, simple option for pasteurization) in foodstuff processing.
  • Conventional planetary roller extruders have to be adapted so that germ and bacteria contamination is kept as low as possible and the regions that come into contact with the foodstuffs can be thoroughly cleaned.
  • the disinfection and acid wash stages can also be carried out in one step.
  • the central aim of other cleaning methods is likewise to avoid having to dismantle systems, which is laborious.
  • the present disclosure provides a planetary roller extruder for homogenizing, dispersing, pasteurizing, and purposefully controlling the temperature of biodegradable materials that are prone to altering their properties during processing, in particular the properties that rule out further use after the materials have been processed, such as food, in particular foodstuffs, or medicinal products or pharmaceutical products, different regions being present in the planetary roller extruder.
  • the planetary roller extruder comprises a flow conduit having various transitions from one region to a next region in an interior of the planetary roller extruder and components being statically and movably installed.
  • the planetary roller extruder comprises a seal installed between statically installed components, by which seal gaps or cavities present are configured to be closed, and a slide ring seal that provides sealing between moving components, which are led from the flow conduit in the interior of the planetary roller extruder outward to a surrounding area, so as to avoid steps and/or notches along flow surfaces in a transition region of the moving components.
  • FIG. 1 shows a planetary roller extruder having a plurality of modules
  • FIG. 2 shows an enlarged region from FIG. 1 ;
  • FIGS. 3 a - 3 c show details from FIG. 2 ;
  • FIG. 4 shows a further enlarged region according to FIG. 1 .
  • a planetary roller extruder for homogenizing, dispersing, pasteurizing, and purposefully controlling the temperature of biodegradable materials that are prone to altering their properties during processing in particular the properties that rule out further use after said materials have been processed, such as food, in particular foodstuffs, or medicinal products or pharmaceutical products, different regions being present in the planetary roller extruder, there being a flow conduit having various transitions from one region to the next region in the interior of the planetary roller extruder, components being statically and movably installed.
  • the present invention provides a planetary roller extruder that can be used for a simple cleaning process and such that no time-consuming dismantling thus needs to be carried out in order to clean the planetary roller extruder. Furthermore, an embodiment of the invention provides a method for carrying out cleaning processes with little or no dismantling of the system components of a planetary roller extruder.
  • An embodiment is characterized in that a seal is installed between statically installed components, by means of which seal gaps or cavities present can be closed, and a slide ring seal provides sealing between moving components, which are led from the flow conduit in the interior of the planetary roller extruder outward to the surrounding area, such as to avoid steps and/or notches along the flow surfaces in the transition region of the moving components. This thus ensures that material does not dwell inside the flow conduit, thereby keeping potential germ formation as low as possible.
  • Elastomer seals, ceramic seals, or metal seals can be used as seals; in this respect, it is important that the seal is deformed such that gaps present with respect to the flow conduit, etc., are closed.
  • the transitions in the flow conduit are configured in terms of flow such that abrupt cross-sectional changes are avoided.
  • At least the regions through which the biodegradable material flows are optimized in terms of flow such that a cleaning medium that flows through permeates all flow spaces.
  • This configuration ensures that, as far as possible, the material flowing through cannot become stuck in the flow conduit.
  • Even just small undercuts, chambers, or conduits provide space in which the materials can dwell in the flow conduit for a relatively long time, thereby allowing germs to form.
  • the configuration of the conduit in terms of flow need not necessarily have a continuous profile in all regions since a turbulent flow can be advantageous in a cleaning process in which a cleaning medium passes through the flow conduit.
  • individual regions be equipped with additional inflow and outflow conduits, as a result of which flow portions can be closed by means of additional components. If protrusions in the flow conduit are unavoidable, for example in regions such as the feed chute, the flow conduit can be closed easily such that a flow surface that is optimized in terms of flow is produced in the roller component. In addition, other regions can in turn be opened if the inflow or outflow of, for example, a cleaning medium in that region is expedient.
  • a method according to an embodiment for cleaning a flow conduit, through which biodegradable material flows, in a planetary roller extruder is characterized in that the flow conduit is flushed using a cleaning medium, all the flow spaces in the flow conduit being permeated by the cleaning medium, or flow surfaces in the flow conduit being heated such that remnants of the biodegradable material combust.
  • the planetary roller extruder is thus configured such that the flow conduit can be cleaned without any dismantling. Any small accumulations of the processed material, as a result of which germs can form, are washed away by means of the cleaning medium or are combusted in a similar way to pyrolysis. Caustic solutions having particular pH values are used as the cleaning medium.
  • a gaseous medium such as water vapor or other media that are in a gaseous state of matter at a temperature that kills germs, flows through the system.
  • a gaseous medium such as water vapor or other media that are in a gaseous state of matter at a temperature that kills germs
  • Caustic solutions, peroxide, disinfectants, etc. are generally not heated; for this reason, a cleaning cycle made up of a plurality of cleaning agents can also be provided, for example pre-cleaning using chemical media, flushing using water, followed by a germ-killing cycle using hot water or water vapor.
  • the cleaning medium is conveyed through the flow conduit at a predetermined temperature and/or a predetermined flow rate.
  • the cleaning medium has to be conveyed through the flow conduit at different temperatures in order to kill germs and/or detach remaining material particles.
  • the flow rate can also play a role as regards whether particles are entrained and thus flushed out, which is why the flow rate can be varied.
  • the method can be optimized by varying the intervals at which media flow through the flow conduit and/or by cleaning individual portions of the flow conduit differently.
  • the planetary roller extruder can be started up, thereby assisting with the dispersal of the cleaning medium. Different operating speeds of the planetary roller extruder during the cleaning can likewise have a positive impact on the cleaning process.
  • the method can thus be adapted to the particular demands of the cleaning process.
  • Various parameters such as the number of flow cycles, the speed of the cleaning medium, its temperature, etc., can be varied. If a laminar or turbulent course of the cleaning medium as it flows through the system is more expedient, this can likewise be achieved by selecting suitable parameter settings. Open-loop or closed-loop control of the process by adjusting the parameters can also be carried out in a fully and/or semi-automatic way by means of the machine controller.
  • the flow conduit can be configured such that the flow surfaces are heated so that all the remnants combust, in a similar way to pyrolysis in ovens. Germs are killed, and only the remaining ash or soot particles need removing; this is ensured by means of a simple flushing operation. Microwave irradiation and/or shaking in the presence of high-frequency radiation can also be provided.
  • FIG. 1 shows a planetary roller extruder 1 in which a plurality of roller components 3 are arranged along the extrusion axis 12 , thus forming zones that are passed through one after the other during the process.
  • the number of zones is determined by the particular application, for example the extent to which thermal or mechanical homogenization is required, or the number of different steps due to heating and cooling, or the gradual admixing of further substances.
  • some roller components 3 have openings 4 , which are closed by a lid but can, if required, be equipped with additional components.
  • One of the openings 4 is equipped with a feed chute 5 , via which materials or additives are fed in.
  • the joint central spindle is driven by means of the drive 2 .
  • the area surrounding the planetary roller extruder 1 is denoted by the reference numeral 16 .
  • the entire system is on a platform, which in turn has height-adjustable system feet 14 .
  • system feet 14 By means of these system feet 14 , for example, a cleaning process can be assisted by tilting the system to a particular angle or swiveling it back and forth in a similar way to a shaking process.
  • FIGS. 2 and 4 are denoted by reference numerals 6 and 7 .
  • FIG. 2 shows the enlargement X having reference numeral 6 according to FIG. 1 , together with a detail Y as reference numeral 8 , which is reproduced in FIG. 3 .
  • the enlargement 6 clearly shows that roller components 3 are arranged one behind the other and are interconnected by means of baffle rings 13 .
  • the interior of the planetary roller extruder 1 is denoted by reference numeral 15
  • the surrounding area is denoted by reference numeral 16 , as in FIG. 1 .
  • FIG. 3 shows the detail according to reference numeral 8 in FIG. 2 .
  • FIGS. 3 a and 3 b differ merely in that FIG. 3 a is configured without the planetary spindle 9 and FIG. 3 b is configured with it.
  • a flow conduit extends in the extrusion direction and continues around the planetary spindle 9 by a first sub-conduit 11 a , via a region 11 b , which in particular includes the contact surface on the baffle ring 13 , and via a transition region 11 c to the next roller component 3 .
  • a longitudinal bore (parallel to the extrusion axis 12 and perpendicular to the contact surface) through the baffle ring 13 can create an additional connection between two adjacent roller components 3 and can thus form a further region of the flow conduit 11 .
  • this again has an impact on the change in the cross section in the flow conduit and can influence it accordingly.
  • this flow conduit 11 is configured such that it can be cleaned by means of a cleaning process, for example the above-described CIP processes, without dismantling the components. Consequently, the flow surfaces of the flow conduit in particular do not have any steps or notches at or between the flow surfaces. Abrupt cross-sectional changes are avoided but are not entirely ruled out; they can even be desirable in some cases for changing the flow behavior, e.g., to achieve a turbulent flow.
  • the transition should, however, be largely homogeneous, i.e., without steps and edges that could again be prone to dirt accumulations.
  • the seals 10 between the static components are also configured accordingly for this purpose and eliminate such steps and/or edges owing to their elasticity.
  • FIG. 4 reproduces the enlargement Z according to reference numeral 7 .
  • one of the roller components 3 having an opening 4 is shown.
  • a feed chute 5 having a lid is placed on said opening 4 , and material can be fed in via said feed chute.
  • the recitation of “at least one of A, B and C” should be interpreted as one or more of a group of elements consisting of A, B and C, and should not be interpreted as requiring at least one of each of the listed elements A, B and C, regardless of whether A, B and C are related as categories or otherwise.
  • the recitation of “A, B and/or C” or “at least one of A, B or C” should be interpreted as including any singular entity from the listed elements, e.g., A, any subset from the listed elements, e.g., A and B, or the entire list of elements A, B and C.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Abstract

A planetary roller extruder for homogenizing, dispersing, pasteurizing, and purposefully controlling the temperature of biodegradable materials that are prone to altering their properties during processing, in particular the properties that rule out further use after the materials have been processed, such as food, medicinal products or pharmaceutical products, different regions being present in the planetary roller extruder. The planetary roller extruder includes a flow conduit having various transitions from one region to a next region in an interior and components being statically and movably installed. A seal is installed between statically installed components, by which seal gaps or cavities present are configured to be closed. A slide ring seal provides sealing between moving components, which are led from the flow conduit in the interior outward to a surrounding area, so as to avoid steps and/or notches along flow surfaces in a transition region of the moving components.

Description

CROSS REFERENCE TO RELATED APPLICATIONS
This application is a U.S. National Phase application under 35 U.S.C. § 371 of International Application No. PCT/EP2022/076167, filed on Sep. 21, 2022, and claims benefit to German Patent Application No. DE 10 2021 125 395.0, filed on Sep. 30, 2021. The International Application was published in German on Apr. 6, 2023 as WO 2023/052211 A1 under PCT Article 21 (2).
FIELD
The invention relates to a planetary roller extruder for homogenizing, dispersing, pasteurizing, and purposefully controlling the temperature of biodegradable materials that are prone to altering their properties during processing. The invention also relates to a method for cleaning the planetary roller extruder.
BACKGROUND
It is well known to use planetary roller extruders to produce a plastics melt, preferably for the granulation process or for continuous film production. In said planetary roller extruders, a plurality of planetary spindles are arranged between a planetary roller cylinder and a central or main spindle.
When the central spindle is driven, the teeth set into the roller cylinders, planetary spindles, and central spindle roll on one another such that the plastics material to be gelled is subject to an intensive kneading action. The plastics melt thus produced is of a high quality.
In addition to the calender-like rolling-out effect in the teeth, the functioning of a planetary roller extruder in terms of a process is determined substantially by the temperature control of the stationary outer casing of the planetary roller cylinder and of the rotating main spindle, since the high surface-area-to-volume ratio in this case can have a particularly effective impact on the preparation of the product.
Therefore, conventional planetary roller cylinders and central spindles are often temperature-controlled internally using a liquid. The temperature profile of the planetary spindles co-rotating between the outer casing and the main spindle cannot be influenced by external measures. In a planetary roller extruder as proposed in DE 37 12 749, the central spindle is cooled. Since the thin melt layers that come into contact with cooled components are repeatedly rearranged, effective and extremely homogeneous cooling is achieved.
The main field of application of the planetary roller extruder is in the preparation of shear- and temperature-sensitive materials, mainly PVC formulations, powder coating binder resins, and thermoplastic polyolefins (TPO). If excessively heated, PVC, for example, reacts by combusting and decomposing. The resulting so-called black spots lead to a considerable degradation in quality, particularly in the case of transparent mixtures or thin films. This problem is alleviated by setting low housing temperatures or by reducing the output by lowering the speeds, which of course results in corresponding efficiency losses.
Powder coatings have to be prepared at the lowest possible temperatures owing to the required dispersibility in pigmented formulations and the risk of crosslinking in transparent, clear formulations. In this case, local excessive heating can likewise accordingly impact on quality, or may render preparation entirely impossible. In this regard, it has been observed that with critical materials (e.g., soft PVC), degradation of the material due to decomposition occurred particularly at the downstream-facing end of the planetary roller component.
When preparing thermoplastic polyolefins, the aim is to achieve uniform melting. For system-related reasons, only a relatively slight pressure can be built up in a planetary roller extruder compared with other preparation systems; this may be advantageous for other forms of preparation.
The goal is to make use of these significant advantages of a planetary roller extruder (good homogenization, good dispersal of the material, simple option for pasteurization) in foodstuff processing. Conventional planetary roller extruders have to be adapted so that germ and bacteria contamination is kept as low as possible and the regions that come into contact with the foodstuffs can be thoroughly cleaned.
In this regard, the so-called CIP (clean-in-place) method has become established. According to Wikipedia, CIP cleaning is defined as a method for cleaning a processing system in situ.
Wikipedia describes the method and sequence as follows:
As the name suggests, in this cleaning method the system is cleaned without substantially dismantling the surfaces that have been in contact with the product. By precisely defining cleaning agents, pressures, temperatures, and times, a reproducible process is established. Clean-in-place was originally developed for the food and dairy product industry.
Conventionally, flushing methods and system sterilization by boiling are used for this purpose.
CIP sequence in the food industry:
    • Pre-rinse to remove coarse residue.
    • Clean with an alkaline agent (possibly with additives to aid the suspension of the dirt particles).
    • Flush cleaning agent out with water.
    • Wash with acid solution to remove limescale and leachate.
    • Flush acid out.
    • Disinfect to kill vegetative micro-organisms.
    • Flush disinfectant out, e.g., with ultrapure water.
The disinfection and acid wash stages can also be carried out in one step.
The central aim of other cleaning methods is likewise to avoid having to dismantle systems, which is laborious.
SUMMARY
In an embodiment, the present disclosure provides a planetary roller extruder for homogenizing, dispersing, pasteurizing, and purposefully controlling the temperature of biodegradable materials that are prone to altering their properties during processing, in particular the properties that rule out further use after the materials have been processed, such as food, in particular foodstuffs, or medicinal products or pharmaceutical products, different regions being present in the planetary roller extruder. The planetary roller extruder comprises a flow conduit having various transitions from one region to a next region in an interior of the planetary roller extruder and components being statically and movably installed. The planetary roller extruder comprises a seal installed between statically installed components, by which seal gaps or cavities present are configured to be closed, and a slide ring seal that provides sealing between moving components, which are led from the flow conduit in the interior of the planetary roller extruder outward to a surrounding area, so as to avoid steps and/or notches along flow surfaces in a transition region of the moving components.
BRIEF DESCRIPTION OF THE DRAWINGS
Subject matter of the present disclosure will be described in even greater detail below based on the exemplary figures. All features described and/or illustrated herein can be used alone or combined in different combinations. The features and advantages of various embodiments will become apparent by reading the following detailed description with reference to the attached drawings, which illustrate the following:
FIG. 1 shows a planetary roller extruder having a plurality of modules;
FIG. 2 shows an enlarged region from FIG. 1 ;
FIGS. 3 a-3 c show details from FIG. 2 ; and
FIG. 4 shows a further enlarged region according to FIG. 1 .
DETAILED DESCRIPTION
In an embodiment, a planetary roller extruder is provided for homogenizing, dispersing, pasteurizing, and purposefully controlling the temperature of biodegradable materials that are prone to altering their properties during processing in particular the properties that rule out further use after said materials have been processed, such as food, in particular foodstuffs, or medicinal products or pharmaceutical products, different regions being present in the planetary roller extruder, there being a flow conduit having various transitions from one region to the next region in the interior of the planetary roller extruder, components being statically and movably installed.
In an embodiment, the present invention provides a planetary roller extruder that can be used for a simple cleaning process and such that no time-consuming dismantling thus needs to be carried out in order to clean the planetary roller extruder. Furthermore, an embodiment of the invention provides a method for carrying out cleaning processes with little or no dismantling of the system components of a planetary roller extruder.
An embodiment is characterized in that a seal is installed between statically installed components, by means of which seal gaps or cavities present can be closed, and a slide ring seal provides sealing between moving components, which are led from the flow conduit in the interior of the planetary roller extruder outward to the surrounding area, such as to avoid steps and/or notches along the flow surfaces in the transition region of the moving components. This thus ensures that material does not dwell inside the flow conduit, thereby keeping potential germ formation as low as possible.
Elastomer seals, ceramic seals, or metal seals can be used as seals; in this respect, it is important that the seal is deformed such that gaps present with respect to the flow conduit, etc., are closed.
According to an embodiment, it is provided that the transitions in the flow conduit are configured in terms of flow such that abrupt cross-sectional changes are avoided.
Alternatively, at least the regions through which the biodegradable material flows are optimized in terms of flow such that a cleaning medium that flows through permeates all flow spaces. This configuration ensures that, as far as possible, the material flowing through cannot become stuck in the flow conduit. Even just small undercuts, chambers, or conduits provide space in which the materials can dwell in the flow conduit for a relatively long time, thereby allowing germs to form. The configuration of the conduit in terms of flow need not necessarily have a continuous profile in all regions since a turbulent flow can be advantageous in a cleaning process in which a cleaning medium passes through the flow conduit.
To improve a cleaning process of this kind, it is provided that individual regions be equipped with additional inflow and outflow conduits, as a result of which flow portions can be closed by means of additional components. If protrusions in the flow conduit are unavoidable, for example in regions such as the feed chute, the flow conduit can be closed easily such that a flow surface that is optimized in terms of flow is produced in the roller component. In addition, other regions can in turn be opened if the inflow or outflow of, for example, a cleaning medium in that region is expedient.
A method according to an embodiment for cleaning a flow conduit, through which biodegradable material flows, in a planetary roller extruder is characterized in that the flow conduit is flushed using a cleaning medium, all the flow spaces in the flow conduit being permeated by the cleaning medium, or flow surfaces in the flow conduit being heated such that remnants of the biodegradable material combust. The planetary roller extruder is thus configured such that the flow conduit can be cleaned without any dismantling. Any small accumulations of the processed material, as a result of which germs can form, are washed away by means of the cleaning medium or are combusted in a similar way to pyrolysis. Caustic solutions having particular pH values are used as the cleaning medium. It is also provided that a gaseous medium, such as water vapor or other media that are in a gaseous state of matter at a temperature that kills germs, flows through the system. In that case, it may not be strictly necessary (depending on the medium) to work with a particular temperature of the medium. Caustic solutions, peroxide, disinfectants, etc. are generally not heated; for this reason, a cleaning cycle made up of a plurality of cleaning agents can also be provided, for example pre-cleaning using chemical media, flushing using water, followed by a germ-killing cycle using hot water or water vapor.
For this purpose, it is provided according to an embodiment that the cleaning medium is conveyed through the flow conduit at a predetermined temperature and/or a predetermined flow rate. Depending on the processed material, the cleaning medium has to be conveyed through the flow conduit at different temperatures in order to kill germs and/or detach remaining material particles. The flow rate can also play a role as regards whether particles are entrained and thus flushed out, which is why the flow rate can be varied.
The method can be optimized by varying the intervals at which media flow through the flow conduit and/or by cleaning individual portions of the flow conduit differently. In addition, the planetary roller extruder can be started up, thereby assisting with the dispersal of the cleaning medium. Different operating speeds of the planetary roller extruder during the cleaning can likewise have a positive impact on the cleaning process. The method can thus be adapted to the particular demands of the cleaning process. Various parameters, such as the number of flow cycles, the speed of the cleaning medium, its temperature, etc., can be varied. If a laminar or turbulent course of the cleaning medium as it flows through the system is more expedient, this can likewise be achieved by selecting suitable parameter settings. Open-loop or closed-loop control of the process by adjusting the parameters can also be carried out in a fully and/or semi-automatic way by means of the machine controller.
Tilting the system out of its horizontal position or moving it back and forth, thereby additionally moving the cleaning medium in the flow conduit, assists the cleaning process.
Further assistance, or even different assistance, for cleaning the flow conduit in the planetary roller extruder is provided. For example, the flow conduit can be configured such that the flow surfaces are heated so that all the remnants combust, in a similar way to pyrolysis in ovens. Germs are killed, and only the remaining ash or soot particles need removing; this is ensured by means of a simple flushing operation. Microwave irradiation and/or shaking in the presence of high-frequency radiation can also be provided.
FIG. 1 shows a planetary roller extruder 1 in which a plurality of roller components 3 are arranged along the extrusion axis 12, thus forming zones that are passed through one after the other during the process. The number of zones is determined by the particular application, for example the extent to which thermal or mechanical homogenization is required, or the number of different steps due to heating and cooling, or the gradual admixing of further substances. For this purpose, some roller components 3 have openings 4, which are closed by a lid but can, if required, be equipped with additional components. One of the openings 4 is equipped with a feed chute 5, via which materials or additives are fed in. The joint central spindle is driven by means of the drive 2. The area surrounding the planetary roller extruder 1 is denoted by the reference numeral 16. The entire system is on a platform, which in turn has height-adjustable system feet 14. By means of these system feet 14, for example, a cleaning process can be assisted by tilting the system to a particular angle or swiveling it back and forth in a similar way to a shaking process. Here, the enlargements reproduced in FIGS. 2 and 4 are denoted by reference numerals 6 and 7.
FIG. 2 shows the enlargement X having reference numeral 6 according to FIG. 1 , together with a detail Y as reference numeral 8, which is reproduced in FIG. 3 . The enlargement 6 clearly shows that roller components 3 are arranged one behind the other and are interconnected by means of baffle rings 13. The interior of the planetary roller extruder 1 is denoted by reference numeral 15, and the surrounding area is denoted by reference numeral 16, as in FIG. 1 .
FIG. 3 shows the detail according to reference numeral 8 in FIG. 2 . FIGS. 3 a and 3 b differ merely in that FIG. 3 a is configured without the planetary spindle 9 and FIG. 3 b is configured with it. A flow conduit extends in the extrusion direction and continues around the planetary spindle 9 by a first sub-conduit 11 a, via a region 11 b, which in particular includes the contact surface on the baffle ring 13, and via a transition region 11 c to the next roller component 3.
A longitudinal bore (parallel to the extrusion axis 12 and perpendicular to the contact surface) through the baffle ring 13 can create an additional connection between two adjacent roller components 3 and can thus form a further region of the flow conduit 11. Depending on the size of this connection, this again has an impact on the change in the cross section in the flow conduit and can influence it accordingly.
In terms of flow, this flow conduit 11 is configured such that it can be cleaned by means of a cleaning process, for example the above-described CIP processes, without dismantling the components. Consequently, the flow surfaces of the flow conduit in particular do not have any steps or notches at or between the flow surfaces. Abrupt cross-sectional changes are avoided but are not entirely ruled out; they can even be desirable in some cases for changing the flow behavior, e.g., to achieve a turbulent flow. The transition should, however, be largely homogeneous, i.e., without steps and edges that could again be prone to dirt accumulations. The seals 10 between the static components are also configured accordingly for this purpose and eliminate such steps and/or edges owing to their elasticity.
FIG. 4 reproduces the enlargement Z according to reference numeral 7. Here, one of the roller components 3 having an opening 4 is shown. A feed chute 5 having a lid is placed on said opening 4, and material can be fed in via said feed chute.
While subject matter of the present disclosure has been illustrated and described in detail in the drawings and foregoing description, such illustration and description are to be considered illustrative or exemplary and not restrictive. Any statement made herein characterizing the invention is also to be considered illustrative or exemplary and not restrictive as the invention is defined by the claims. It will be understood that changes and modifications may be made, by those of ordinary skill in the art, within the scope of the following claims, which may include any combination of features from different embodiments described above.
The terms used in the claims should be construed to have the broadest reasonable interpretation consistent with the foregoing description. For example, the use of the article “a” or “the” in introducing an element should not be interpreted as being exclusive of a plurality of elements. Likewise, the recitation of “or” should be interpreted as being inclusive, such that the recitation of “A or B” is not exclusive of “A and B,” unless it is clear from the context or the foregoing description that only one of A and B is intended. Further, the recitation of “at least one of A, B and C” should be interpreted as one or more of a group of elements consisting of A, B and C, and should not be interpreted as requiring at least one of each of the listed elements A, B and C, regardless of whether A, B and C are related as categories or otherwise. Moreover, the recitation of “A, B and/or C” or “at least one of A, B or C” should be interpreted as including any singular entity from the listed elements, e.g., A, any subset from the listed elements, e.g., A and B, or the entire list of elements A, B and C.
LIST OF REFERENCE NUMERALS
    • 1 Planetary roller extruder
    • 2 Drive
    • 3 Roller component
    • 4 Openings in 3
    • 5 Feed chute
    • 6 Enlargement X
    • 7 Enlargement Z
    • 8 Detail Y
    • 9 Planetary spindle
    • 10 Seal
    • 11 Flow conduit
    • 12 Extrusion axis
    • 13 Baffle ring
    • 14 System foot
    • 15 Inner region of 1
    • 16 Surrounding area

Claims (13)

The invention claimed is:
1. A planetary roller extruder for homogenizing, dispersing, pasteurizing, and purposefully controlling the temperature of biodegradable materials that are prone to altering their properties during processing, including the properties that rule out further use after the materials have been processed, including foodstuffs, or medicinal products or pharmaceutical products, different regions being present in the planetary roller extruder, the planetary roller extruder comprising:
a flow conduit having various transitions from one region to a next region in an interior of the planetary roller extruder;
components being statically and movably installed;
a seal installed between statically installed components, by which seal gaps or cavities present are configured to be closed; and
a slide ring seal that provides sealing between moving components, which are led from the flow conduit in the interior of the planetary roller extruder outward to a surrounding area, so as to avoid steps and/or notches along flow surfaces in a transition region of the moving components.
2. The planetary roller extruder according to claim 1, wherein the transitions in the flow conduit are configured in terms of flow such that abrupt cross-sectional changes are avoided.
3. The planetary roller extruder according to claim 2, wherein at least the regions through which the biodegradable material flows are optimized in terms of flow such that a cleaning medium that flows through permeates all flow spaces.
4. The planetary roller extruder according to claim 3, wherein regions are equipped with additional inlet and outlet conduits.
5. The planetary roller extruder according to claim 3, wherein flow portions can be closed by additional components.
6. A method for cleaning a flow conduit, through which biodegradable material flows, in the planetary roller extruder according to claim 1, the method comprising:
flushing the flow conduit using a cleaning medium; and
permeating all flow spaces in the flow conduit with the cleaning medium, or heating flow surfaces in the flow conduit such that remnants of biodegradable material combust.
7. The method according to claim 6, wherein the cleaning medium is conveyed through the flow conduit at a predetermined temperature and/or a predetermined flow rate.
8. The method according to claim 6, wherein intervals at which media flow through the flow conduit are varied.
9. The method according to claim 6, wherein the flow conduit comprises portions that are cleaned differently.
10. The method according to claim 6, wherein an operating speed of the planetary roller extruder is different during the cleaning.
11. The method according to claim 6, wherein horizontal positions of the planetary roller extruder are changed.
12. The method according to claim 9, wherein the cleaning medium is conveyed through the flow conduit at a predetermined temperature and/or a predetermined flow rate.
13. The method according to claim 9, wherein intervals at which media flow through the flow conduit are varied.
US18/695,818 2021-09-30 2022-09-21 Planetary roller extruder for processing biodegradable materials and method for cleaning the planetary roller extruder Active 2042-12-08 US12552080B2 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE102021125395.0 2021-09-30
DE102021125395.0A DE102021125395A1 (en) 2021-09-30 2021-09-30 Planetary roller extruder for processing biodegradable materials and method for cleaning the planetary roller extruder
PCT/EP2022/076167 WO2023052211A1 (en) 2021-09-30 2022-09-21 Planetary roller extruder for processing biodegradable materials and method for cleaning the planetary roller extruder

Publications (2)

Publication Number Publication Date
US20250018631A1 US20250018631A1 (en) 2025-01-16
US12552080B2 true US12552080B2 (en) 2026-02-17

Family

ID=83995155

Family Applications (1)

Application Number Title Priority Date Filing Date
US18/695,818 Active 2042-12-08 US12552080B2 (en) 2021-09-30 2022-09-21 Planetary roller extruder for processing biodegradable materials and method for cleaning the planetary roller extruder

Country Status (4)

Country Link
US (1) US12552080B2 (en)
EP (1) EP4395974A1 (en)
DE (1) DE102021125395A1 (en)
WO (1) WO2023052211A1 (en)

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3520662A1 (en) 1985-06-08 1987-01-02 Rudolf Paul Fritsch SHAFT SEAL FOR A DEVICE FOR CONTINUOUSLY PROCESSING HIGH VISCOSITY MEDIA, ESPECIALLY FOR THE PRODUCTION OF HIGH MOLECULAR POLYMERS
DE3712749C1 (en) 1987-04-15 1988-07-07 Berstorff Gmbh Masch Hermann Use of a secondary extruder of a tandem system for cooling a plastic blowing agent mixture melt produced in a primary extruder
DE19508125C1 (en) 1995-02-13 1996-02-29 Gewerk Schalker Eisenhuette Induction cylinder for planet roller extruder
WO1997031767A2 (en) 1996-02-29 1997-09-04 Fritsch, Rosemarie, J. Multi-shaft worm machine
DE10142890A1 (en) * 2001-09-03 2003-03-20 Rust & Mitschke Entex Extruder with planetary gear section for processing plastics has a central spindle with cut-away teeth close to the planetary spindle end bearing ring
DE102006063021B3 (en) * 2006-01-16 2018-04-26 Entex Rust & Mitschke Gmbh Planetary roller extruder
DE102019001191A1 (en) * 2018-02-28 2019-08-29 Entex Rust & Mitschke Gmbh Production and processing of polymer blends with other substances by extrusion
EP3594303A1 (en) * 2018-07-12 2020-01-15 Tesa Se Production of an adhesive mass based on solid epdm rubber
DE102020003391A1 (en) 2020-03-19 2021-09-23 E N T E X Rust & Mitschke GmbH 3D printer for making and decorating bakery and confectionery products

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3520662A1 (en) 1985-06-08 1987-01-02 Rudolf Paul Fritsch SHAFT SEAL FOR A DEVICE FOR CONTINUOUSLY PROCESSING HIGH VISCOSITY MEDIA, ESPECIALLY FOR THE PRODUCTION OF HIGH MOLECULAR POLYMERS
US4773654A (en) 1985-06-08 1988-09-27 Fritsch Rudolf P Shaft seal assembly, in particular for an apparatus for continuous processing of very viscous media
DE3712749C1 (en) 1987-04-15 1988-07-07 Berstorff Gmbh Masch Hermann Use of a secondary extruder of a tandem system for cooling a plastic blowing agent mixture melt produced in a primary extruder
DE19508125C1 (en) 1995-02-13 1996-02-29 Gewerk Schalker Eisenhuette Induction cylinder for planet roller extruder
WO1997031767A2 (en) 1996-02-29 1997-09-04 Fritsch, Rosemarie, J. Multi-shaft worm machine
DE10142890A1 (en) * 2001-09-03 2003-03-20 Rust & Mitschke Entex Extruder with planetary gear section for processing plastics has a central spindle with cut-away teeth close to the planetary spindle end bearing ring
DE102006063021B3 (en) * 2006-01-16 2018-04-26 Entex Rust & Mitschke Gmbh Planetary roller extruder
DE102019001191A1 (en) * 2018-02-28 2019-08-29 Entex Rust & Mitschke Gmbh Production and processing of polymer blends with other substances by extrusion
EP3594303A1 (en) * 2018-07-12 2020-01-15 Tesa Se Production of an adhesive mass based on solid epdm rubber
US20200017723A1 (en) 2018-07-12 2020-01-16 Tesa Se Producing a pressure-sensitive adhesive based on solid epdm rubber
DE102020003391A1 (en) 2020-03-19 2021-09-23 E N T E X Rust & Mitschke GmbH 3D printer for making and decorating bakery and confectionery products

Also Published As

Publication number Publication date
DE102021125395A1 (en) 2023-03-30
EP4395974A1 (en) 2024-07-10
US20250018631A1 (en) 2025-01-16
WO2023052211A1 (en) 2023-04-06

Similar Documents

Publication Publication Date Title
AU2009259653B2 (en) Device for producing and filling containers
EP1464342B1 (en) Apparatus and process for sterilising liquids using ultraviolet radiation and short-time heating
RU2535077C2 (en) Uv fluid steriliser
JP4843816B2 (en) Blow molding machine with CIP system for producing plastic bottles, especially PET bottles
CN112079311B (en) Sterilization conversion method and product filling device
JP6644761B2 (en) Mixing element with improved dispersion effect
US12552080B2 (en) Planetary roller extruder for processing biodegradable materials and method for cleaning the planetary roller extruder
CN1774326B (en) multi-screw extruder
CA2743380A1 (en) Uv irradiation apparatus and method
US10488125B2 (en) Scraping heat exchanger
CA3000023C (en) Method for reducing microbiological contaminants of container products
JP2781772B2 (en) Kneading extruder
CN109562535B (en) Apparatus and method for producing dyed and undyed plastic melts
EP3347186B1 (en) Apparatus and method for injecting a fluid formulation into a melted polymeric material
EP2520313A1 (en) Heatable flange
JP4913098B2 (en) Steam sterilizer
US20070066797A1 (en) Apparatus for producing polymer
EP1728565A2 (en) A device for washing containers and method therefor
US9868241B1 (en) Extrusion process for tubular member
JP2001087638A (en) Shaft sealing part of closed stirring apparatus
KR200363666Y1 (en) water purifier
EP4215332A1 (en) Method for recycling and sterilizing thermoplastics from products having same heterogenous composition, and installation for implementing such method
CN121376278A (en) Plugging piece for filling machine and filling pipe assembly
CN119817842A (en) Sterilization and concentration equipment and working method thereof
JP2025504230A (en) Method and plant for recycling plastic waste

Legal Events

Date Code Title Description
AS Assignment

Owner name: BATTENFELD-CINCINNATI GERMANY GMBH, GERMANY

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:GESPER, THOMAS;DOHMANN, HEINRICH;KAISER, MICHAEL;REEL/FRAME:066910/0911

Effective date: 20240321

FEPP Fee payment procedure

Free format text: ENTITY STATUS SET TO UNDISCOUNTED (ORIGINAL EVENT CODE: BIG.); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

STPP Information on status: patent application and granting procedure in general

Free format text: DOCKETED NEW CASE - READY FOR EXAMINATION

STPP Information on status: patent application and granting procedure in general

Free format text: NON FINAL ACTION COUNTED, NOT YET MAILED

STPP Information on status: patent application and granting procedure in general

Free format text: NON FINAL ACTION MAILED

STPP Information on status: patent application and granting procedure in general

Free format text: RESPONSE TO NON-FINAL OFFICE ACTION ENTERED AND FORWARDED TO EXAMINER

STPP Information on status: patent application and granting procedure in general

Free format text: ALLOWED -- NOTICE OF ALLOWANCE NOT YET MAILED

Free format text: NOTICE OF ALLOWANCE MAILED -- APPLICATION RECEIVED IN OFFICE OF PUBLICATIONS

STPP Information on status: patent application and granting procedure in general

Free format text: PUBLICATIONS -- ISSUE FEE PAYMENT RECEIVED

Free format text: PUBLICATIONS -- ISSUE FEE PAYMENT VERIFIED

STCF Information on status: patent grant

Free format text: PATENTED CASE